JPS6247371A - Gas purifier and oxygen enriched gas feeder - Google Patents

Gas purifier and oxygen enriched gas feeder

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Publication number
JPS6247371A
JPS6247371A JP18588585A JP18588585A JPS6247371A JP S6247371 A JPS6247371 A JP S6247371A JP 18588585 A JP18588585 A JP 18588585A JP 18588585 A JP18588585 A JP 18588585A JP S6247371 A JPS6247371 A JP S6247371A
Authority
JP
Japan
Prior art keywords
oxygen
gas
filter
enriched
enriched gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
JP18588585A
Other languages
Japanese (ja)
Other versions
JPH0312901B2 (en
Inventor
杉本 作藏
隆夫 西村
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Teijin Ltd
Original Assignee
Teijin Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Teijin Ltd filed Critical Teijin Ltd
Priority to JP18588585A priority Critical patent/JPS6247371A/en
Publication of JPS6247371A publication Critical patent/JPS6247371A/en
Publication of JPH0312901B2 publication Critical patent/JPH0312901B2/ja
Granted legal-status Critical Current

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  • Respiratory Apparatuses And Protective Means (AREA)
  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 く利用分野〉 本発明は、特定の構造を有した気体浄化器及び気体浄化
器を組み込んだ酸素富化気体供給装置に関する。さらに
詳細には、医療用その他の呼吸改善又は補強のために酸
素富化気体を患者等の使用者の鼻腔や口内に供給するた
めの装置であって、患者の鼻腔内等に供給する前の酸素
富化気体を浄化するための気体浄化器を具備せしめた酸
素富化気体供給装置及びその気体浄化器を提供するもの
である。
DETAILED DESCRIPTION OF THE INVENTION Field of Application The present invention relates to a gas purifier having a specific structure and an oxygen-enriched gas supply device incorporating the gas purifier. More specifically, it is a device for supplying oxygen-enriched gas to the nasal cavity or mouth of a user such as a patient for medical or other purposes to improve or strengthen breathing, The present invention provides an oxygen-enriched gas supply device equipped with a gas purifier for purifying oxygen-enriched gas, and the gas purifier.

〈従来技術〉 従来、呼吸器疾患患者に対して酸素ボンベや液体酸素等
から酸素を供給する酸素療法が行われており、最近では
空気中の酸素を濃縮して得られた酸素富化空気を使用し
た酸素療法が開発されることによってその治療法が次第
に酋及するようになって来ている。
<Prior art> Oxygen therapy, which supplies oxygen from oxygen cylinders or liquid oxygen, has traditionally been used for patients with respiratory diseases, and recently oxygen-enriched air obtained by concentrating oxygen in the air has been used With the development of oxygen therapy, this treatment has become increasingly popular.

これらの酸素療法では、酸素や酸素富化空気等の気体を
患者の鼻腔に供給する際、患者の鼻腔内の乾燥を防止す
るために通常は飽和水蒸気圧近くまで加湿した状態でそ
の気体を供給するように工夫がなされている。即ち酸素
ガスボンベや液体酸素等からの酸素の場合には、そのま
までは湿度が低すぎるために例えば気泡形式の加湿器等
を通過せしめて加湿した後に患者に供給される。また酸
素富化空気を得るために、吸着型酸素富化器や成型酸素
富化器が使用されるが、この吸着型酸素富化器の場合に
も通常得られる酸素富化空気に水分がほとんど含まれな
いために加湿器を用いて加湿せしめた富化空気が患者に
供給される。尚成型酸素富化器の場合には通常該膜より
水分が濃縮されるために特に加湿器を設ける必要のない
ことが多い。
In these oxygen therapies, when gases such as oxygen or oxygen-enriched air are supplied to the patient's nasal cavity, the gas is usually supplied in a humidified state close to the saturated water vapor pressure to prevent the patient's nasal cavity from drying out. Efforts have been made to do so. That is, in the case of oxygen from an oxygen gas cylinder or liquid oxygen, the humidity is too low as it is, so it is supplied to the patient after being humidified, for example, by passing through a bubble type humidifier. In addition, adsorption type oxygen enrichers and molded oxygen enrichers are used to obtain oxygen-enriched air, but even in the case of adsorption type oxygen enrichers, the oxygen-enriched air that is usually obtained contains almost no moisture. The patient is provided with enriched air that is humidified using a humidifier. In the case of a molded oxygen enricher, it is often unnecessary to provide a humidifier because water is usually concentrated in the membrane.

この様に加湿器や膜等により湿度が高められた酸素又は
酸素富化空気等の気体は、例えば塩化ビニール製等のチ
ューブ内を流通せしめ、離れた場所に位置する患者の0
腔や口内に鼻カニユーラ。
In this way, gases such as oxygen or oxygen-enriched air whose humidity has been increased using a humidifier or membrane are passed through tubes made of vinyl chloride, etc.
Nasal cannula in cavity and mouth.

マスク等を介して供給されるが、該気体がチューブを通
過する際に冷却されて結露し、水滴となって患者の鼻腔
等に達する為に患者に不快感を与えたり、バクテリア等
が繁殖しやすいなどの衛生上の問題点があった。
The gas is supplied through a mask, etc., but as it passes through the tube, it cools and condenses, forming water droplets that reach the patient's nasal cavity, causing discomfort to the patient and causing bacteria to grow. There were hygienic issues such as easy cleaning.

また上記の如く気体をチューブ内を通過せしめる際や、
その前の酸素富化器を通過せしめる際等に、例えば該チ
ューブを構成する塩化ビニール中に含まれる可塑剤など
が微かながらも蒸発揮散して気体中に混入する場合があ
り、それが患者にとって異臭と感じられ不快感を与える
欠点があった。
Also, when gas is passed through the tube as mentioned above,
When passing through the oxygen enricher in front of the tube, for example, a small amount of plasticizer contained in the vinyl chloride that makes up the tube may evaporate and be mixed into the gas, which may be harmful to the patient. There was a drawback that it was perceived as a strange odor and caused discomfort.

〈発明の目的〉 本発明は、上記の問題点を解決することを目的としてお
り、特に酸素や酸素富化空気等の気体が患者の鼻腔等に
入る前にその中に含まれる水滴や異臭原因物質を除去し
、出来るだけ正常な気体を患者に供給し得る酸素富化気
体供給装置、及びそれに使用され得る気体浄化器を提供
することを目的としている。
<Purpose of the Invention> The present invention aims to solve the above-mentioned problems, and in particular, eliminates water droplets contained in gases such as oxygen and oxygen-enriched air before they enter the patient's nasal cavity, which causes odor. It is an object of the present invention to provide an oxygen-enriched gas supply device that can remove substances and supply as normal a gas as possible to a patient, and a gas purifier that can be used therein.

〈発明の構成〉 かかる目的を達成すべく鋭意研究した結果、酸素富化気
体を患者等のの腔に供給する際に出来るだけ使用者の近
くにおいて該気体を浄化せしめる気体浄化器を具備せし
めることが有効であることを見い出し本発明に到達した
。
<Structure of the Invention> As a result of intensive research to achieve the above object, we have provided a gas purifier that purifies oxygen-enriched gas as close to the user as possible when supplying the gas to the cavity of a patient, etc. The inventors have discovered that this is effective and have arrived at the present invention.

即ち本発明は、気体の入口及び出口を具備した容器内に
フィルターと吸着剤層を直列に配した気体浄化器:及び
該発生手段から離れて位置した酸素富化気体の発生手段
と、該酸素富化気体を使用に供する供給手段と、該発生
手段から該供給手段に該酸素富化気体を導くための導管
手段を有した酸素富化気体供給装置であって、該導管手
段の途中にフィルター及び/又は吸着剤を具備した気体
浄化手段を有したことを特徴とする酸素富化気体供給装
置を提供する。
That is, the present invention provides a gas purifier having a filter and an adsorbent layer arranged in series in a container equipped with a gas inlet and an outlet; An oxygen-enriched gas supply apparatus comprising supply means for supplying enriched gas and conduit means for guiding the oxygen-enriched gas from the generation means to the supply means, the conduit having a filter in the middle thereof. The present invention provides an oxygen-enriched gas supply device characterized by having a gas purification means equipped with an adsorbent and/or an adsorbent.

以下本発明について図面を用いてさらに詳細に説明する
。本発明における酸素富化気体供給装置の好ましい態様
は、第1図に模式的に例示する如く、酸素富化気体発生
手段1から酸素富化気体が加湿器3を通過して加湿され
た後、導管手段5を通過し、次いで吸着剤9及びフィル
ター11を内蔵した気体浄化手段7を通ることによって
その直前までに該富化気体中に含まれる水滴や臭気源等
の不純物が除去されて、更に導管手段を経た後、浄化さ
れた酸素富化気体が供給手段13より使用者の^腔内1
5に供給されるようにしたものである。
The present invention will be explained in more detail below with reference to the drawings. In a preferred embodiment of the oxygen-enriched gas supply device according to the present invention, as schematically illustrated in FIG. Immediately before passing through the conduit means 5 and then through the gas purification means 7 containing an adsorbent 9 and a filter 11, impurities such as water droplets and odor sources contained in the enriched gas are removed. After passing through the conduit means, the purified oxygen-enriched gas is delivered to the user's cavity 1 from the supply means 13.
5.

本発明の酸素富化気体供給装置は、富化気体発生手段で
ある酸素ボンベ等又は酸素富化手段を収納した酸素富化
器から離れた場所において該富化気体を使用に供する供
給手段を用いる際に、酸素富化器や酸素ボンベ等から供
給手段までの導管手段の間にフィルター及び/又は吸着
剤を収納した気体浄化手段を有したことを特徴としてい
る。
The oxygen-enriched gas supply device of the present invention uses a supply means that makes the enriched gas available at a location away from an oxygen cylinder or the like that is the enriched gas generation means or an oxygen enricher housing the oxygen enrichment means. In particular, it is characterized by having a gas purification means containing a filter and/or an adsorbent between the conduit means from the oxygen enricher, oxygen cylinder, etc. to the supply means.

かかるフィルターとしては、それ以前の導管手段や酸素
富化気体発生手段で発生した水滴の通過を防ぐ機能を有
したものが好ましく、そのためには平径孔径が0.8μ
以下のもの、更に好ましくは0.7μ以下のものを用い
ることが望ましい。また該フィルターとしては、セルロ
ース系、ガラス繊維、ポリエステル系等を含むいかなる
ものでもよいが、その少なくとも上流側の面で撥水性を
保持したもの方が水滴通過阻止のうえで好ましい。撥水
性を保持せしめるには、フィルターの素材に例えば四フ
ッ化エチレン樹脂等のフッ素系樹脂、シリコーン系樹脂
、ポリオレフィン系樹脂等の疎水性材料を用いることが
でき、特にフッ素系樹脂が撥水効果や成形性において優
れている。また撥水性を有したフィルターとして、撥水
性のない素材からなるフィルターの片面又は両面に撥水
処理を施したものを用いることもできる。その撥水処理
に用いられる撥水剤として(4いかなるものであっても
よく、例えばフッ素系あるいはシリコーン系の樹脂等の
1發水剤を、含浸、散布、塗布あるいは蒸着法等によっ
て処理せしめたフィルターが使用できる。
It is preferable that such a filter has the function of preventing the passage of water droplets generated by the previous conduit means or oxygen-enriched gas generation means.
It is desirable to use the following materials, more preferably 0.7 μm or less. The filter may be of any type, including cellulose, glass fiber, polyester, etc., but it is preferable to use one that retains water repellency at least on its upstream surface in order to prevent water droplets from passing through. In order to maintain water repellency, hydrophobic materials such as fluorine resins such as tetrafluoroethylene resin, silicone resins, and polyolefin resins can be used as filter materials. In particular, fluorine resins have a water repellent effect. It has excellent moldability and moldability. Further, as a water-repellent filter, a filter made of a non-water-repellent material and subjected to water-repellent treatment on one or both sides can also be used. The water repellent used for the water repellent treatment (4) may be of any kind, for example, 1 water repellent such as fluorine-based or silicone-based resin, and treated by impregnation, spraying, coating, or vapor deposition. Filters can be used.

また該フィルターは、例えば導管手段の下流側からバク
テリアが侵入し、フィルターの上流側に入り込んで繁殖
することを防止するだめの除菌フィルターとして用いら
れることが可能であり、そのためにはその細孔系が0.
5μ以下が好ましく、より確実には0.3μ以下が望ま
しい。
The filter can also be used as a sterilization filter, for example to prevent bacteria from entering from the downstream side of the conduit means and entering the upstream side of the filter and multiplying. The system is 0.
The thickness is preferably 5μ or less, more certainly 0.3μ or less.

尚、該フィルターの形状としてはいかなるものであって
もよいが、全体として酸素富化気体が通過、する際の圧
力損失が小さいものが好ましい。さらに具体的には、例
えば酸素富化気体の流量が61 /n1inの場合の該
フィルタ一部での圧力損失が20mHO以下で更に好ま
しくは16+1!IIIH(]以下あることが望ましい
。
The shape of the filter may be any shape, but it is preferable that the pressure loss as a whole is small when the oxygen-enriched gas passes through it. More specifically, for example, when the flow rate of the oxygen-enriched gas is 61/n1in, the pressure loss at a portion of the filter is 20 mHO or less, more preferably 16+1! It is desirable that it be less than or equal to IIIH(].

また本発明の前記気体浄化器に用いられる吸着剤として
は、例えば導管手段5として塩化ビニール製のチューブ
を用いた場合にその内部を流通する酸素富化気体に混入
してくるフタル酸エステル等の異臭源や、場合によって
は酸素富化器中で発生した異臭源等を吸着し得るもので
あればいかなるものであってもよい。その具体例として
は、モレキュラーシーブ5A等のゼオライト、活性炭。
Further, as the adsorbent used in the gas purifier of the present invention, for example, when a vinyl chloride tube is used as the conduit means 5, phthalate esters etc. that are mixed into the oxygen-enriched gas flowing inside the tube are used. Any material may be used as long as it can adsorb sources of off-odor or, in some cases, off-odor sources generated in the oxygen enricher. Specific examples include zeolites such as molecular sieve 5A, and activated carbon.

フロリジル等があげられ、中でも活性炭やゼオライトが
好ましい。
Examples include florisil, among which activated carbon and zeolite are preferred.

本発明の酸素富化気体供給装置の導管手段5に具備せし
める気体浄化手段としては、第1図に例示した如くフィ
ルターと吸着剤の両方を用いたものが最も好ましいが、
場合によっては該気体浄化手段として吸着剤又はフィル
ターのどちらか一方のみを収納したものであってもよい
。さらにフィルターと吸着剤の両方を用いた気体浄化手
段の場合には、各々を別々の容器に収納せしめてもよい
が、たとえば第2図に示す如く1つの容器19内にフィ
ルター11と吸着剤9の両方を収納したものの方が全体
を小さく軽量にできるので好ましい。尚第2図中、11
は充填した吸着剤を封じこめるための繊維集合体等から
なる栓である。またフィルターと吸着剤は直列に配した
ものが好ましく、その順序としては、フィルターを下流
側に用いた方が下流側からのバクテリアの侵入を防止で
きまた吸着剤の破片等の固型物が下流側に流出すること
もないので好ましい。但し異臭が激しい場合には、吸着
剤が水滴により不活性化されてその吸着能が低下するこ
とを防ぐためにフィルターを上流側に配したものを用い
ることが望ましい。また圧力損失が少なくできれば、吸
着剤の前後にフィルターを配したものが良い。さらに該
気体浄化手段を具備せしめる位置としては、導管手段5
のより下流側の方がその効果を発揮しやすい。特に酸素
富化気体の供給手段13のできるだけ直前に気体浄化手
段を設けるのが望ましいが、あまりに近すぎるとその供
給手段を使用する者に不都合を生ずるので、その場合に
は例えば該気体浄化手段を使用者の肩にかけたり胸部等
に固定するようにしたものが望ましい。尚、該富化器が
、内部の導管手段に吸着剤や除菌フィルターを具備せし
めたものであってもよい。
As the gas purification means provided in the conduit means 5 of the oxygen-enriched gas supply device of the present invention, it is most preferable to use both a filter and an adsorbent as illustrated in FIG.
In some cases, the gas purifying means may include only either an adsorbent or a filter. Furthermore, in the case of a gas purification means that uses both a filter and an adsorbent, each may be stored in separate containers, but for example, as shown in FIG. It is preferable to use a device that stores both of the above because it can make the entire device smaller and lighter. In addition, 11 in Figure 2
is a stopper made of a fiber aggregate or the like to confine the filled adsorbent. In addition, it is preferable to arrange the filter and adsorbent in series; using the filter on the downstream side will prevent bacteria from entering from the downstream side, and will also prevent solid objects such as adsorbent fragments from downstream. This is preferable because it does not leak to the sides. However, if there is a strong odor, it is desirable to use a filter disposed on the upstream side to prevent the adsorbent from being inactivated by water droplets and reducing its adsorption capacity. Also, if pressure loss can be reduced, it is better to place filters before and after the adsorbent. Further, as a position where the gas purification means is provided, the conduit means 5
The effect is more likely to be exerted on the downstream side. In particular, it is desirable to provide the gas purification means immediately before the oxygen-enriched gas supply means 13, but if it is too close, it will cause inconvenience to the person using the supply means. It is desirable to have one that can be hung over the user's shoulder or fixed to the chest, etc. Incidentally, the enrichment device may be one in which the internal conduit means is equipped with an adsorbent or a sterilization filter.

本発明の酸素富化気体供給装置における酸素富化気体発
生手段の具体例としては、膜型酸素富化器、吸着型酸素
富化器等の空気中から酸素富化空気を得る酸素富化器、
酸素ボンベ及び液体酸素から酸素ガスを得る手段等の1
種を用いたもの又はそれらを組み合わせたものがあげら
れる。この様に本発明で言う酸素富化気体とは、酸素富
化空気や酸素ガスを意味する。
Specific examples of the oxygen-enriched gas generation means in the oxygen-enriched gas supply device of the present invention include oxygen enrichers that obtain oxygen-enriched air from air, such as membrane-type oxygen enrichers and adsorption-type oxygen enrichers. ,
1. Means for obtaining oxygen gas from oxygen cylinders and liquid oxygen, etc.
Examples include those using seeds or a combination of them. As described above, the term "oxygen-enriched gas" as used in the present invention means oxygen-enriched air or oxygen gas.

また膜型酸素富化器とは、酸素選択透過性膜に空気を透
過させて酸素富化空気を得るものであり、通常は酸素と
共に水分が濃縮される場合にはさらに加湿器を具備せし
める必要はなく、逆に濃縮された水分が器内で凝縮して
水滴となるために水分離手段を具備することが望ましい
。その様にして)qられた酸素富化空気は約70%以上
の相対湿度の水分を含んでいるために該富化器から延長
された導管手段内で冷却されてい再度水滴が発生しやす
いことから、前記の如き気体浄化手段を具備せしめるこ
とが必要である。
In addition, a membrane-type oxygen enricher is a device that obtains oxygen-enriched air by passing air through an oxygen-selective permeable membrane, and usually requires a humidifier if moisture is concentrated along with oxygen. On the contrary, the concentrated water condenses into water droplets within the vessel, so it is desirable to provide a water separation means. Since the oxygen-enriched air thus obtained contains moisture with a relative humidity of about 70% or more, it is likely to be cooled in the conduit means extended from the enricher and water droplets will be generated again. Therefore, it is necessary to provide a gas purifying means as described above.

吸着型酸素富化器は、酸素と窒素の吸着能の差がある吸
着剤を用いて空気中より酸素富化空気を1qるものであ
るが、この際に水分も分離されて該富化空気が乾燥され
る場合にさらに加湿器を句加することが必要である。ま
た酸素ボンベ等から酸素ガスを得る場合にはも、通常は
加湿式を設けたものが好ましい。この様に加湿器として
用いられものの形式等はいかなるものであってもよく、
第1図の3に示す如く水4を充填して気泡2を発生させ
る形式のものが実用的である。加湿器から出て来る酸素
富化気体中の相対湿度は約70%以上であることが望ま
しく、その湿度の制御方法として気泡の表面積を調節す
ること、さらに具体的には加湿器内の水充填部の横断面
積を調節して上昇し破裂する気泡数を制御することが有
効である。この様にして得られる湿度が約70%以上特
に80%以上の酸素富化気体は、前記と同様に加湿器か
ら下流に延長された導管手段内で冷却されて水滴を生じ
やすく、該導管手段内に前記の気体浄化手段を設ける必
要がある。
An adsorption type oxygen enricher uses an adsorbent that has a difference in adsorption capacity for oxygen and nitrogen to obtain 1 q of oxygen-enriched air from the air.At this time, water is also separated and the enriched air is It is necessary to add a humidifier when the air is dried. Also, when obtaining oxygen gas from an oxygen cylinder or the like, it is usually preferable to use a humidifier. In this way, any type of humidifier can be used,
Practical is a type in which air bubbles 2 are generated by filling water 4 as shown in 3 in FIG. The relative humidity in the oxygen-enriched gas coming out of the humidifier is preferably about 70% or more, and the humidity can be controlled by adjusting the surface area of the air bubbles, and more specifically by filling the humidifier with water. It is effective to control the number of bubbles that rise and burst by adjusting the cross-sectional area of the section. The oxygen-enriched gas having a humidity of about 70% or more, particularly 80% or more, obtained in this way is likely to be cooled and form water droplets in the conduit means extending downstream from the humidifier, as described above, and the conduit means It is necessary to provide the above-mentioned gas purification means inside the tank.

また本発明の酸素富化気体供給装置における導管手段と
しては、軟質プラスチック材料からなるチューブが好ま
しく、例えば軟質塩化ビニール。
Further, as the conduit means in the oxygen-enriched gas supply device of the present invention, a tube made of a soft plastic material is preferable, such as soft vinyl chloride.

シリコーンゴム、ポリオレフィン、ポリスチレン。silicone rubber, polyolefin, polystyrene.

テフロン等からなるもの挙げられる。これらの中でも、
異臭の発生がより少ない素材からなるものが好ましく、
その例としてはポリオレフィン、ポリスチレンからなる
ものがあげられる。尚この様な素材からなるチューブを
用いた場合であっても、本発明に言う気体浄化手段を用
いなければそれを用いる患者にとって異臭が気になる場
合が考えられる。
Examples include those made of Teflon and the like. Among these,
It is preferable to use a material that produces less off-odor.
Examples include those made of polyolefin and polystyrene. Even when a tube made of such a material is used, if the gas purification means of the present invention is not used, the patient using the tube may experience an unpleasant odor.

さらに本発明の装置における酸素富化気体を使用に供す
る供給手段の形式はいかなるものであってもよく、その
具体例としての腔内に細いチューブの先端を挿入するの
カニューラ形式やマスク形式のものがあげられる。かか
る供給手段から供給される酸素富化気体の流量としては
、その発生手段として酸素富化器を用いた場合、下限が
0.1fi/min 、更にはo、5p /min 、
特に1μ/minであることが好ましく、また上限とし
ては10U/min、更には31/min、特に61/
minであることが望ましい。
Further, the supply means for supplying oxygen-enriched gas in the device of the present invention may be of any type, and specific examples thereof include a cannula type in which the tip of a thin tube is inserted into a cavity, and a mask type. can be given. As for the flow rate of the oxygen-enriched gas supplied from such a supply means, when an oxygen enricher is used as the generation means, the lower limit is 0.1 fi/min, more preferably o, 5 p/min,
In particular, it is preferably 1μ/min, and the upper limit is 10U/min, more preferably 31/min, especially 61/min.
It is desirable that it be min.

本発明の?!2素富化器の好ましい態様の1つである膜
型酸素富化器の具体的構造を次に例示する。
The invention? ! A specific structure of a membrane type oxygen enricher, which is one of the preferred embodiments of the diatomic enricher, will be illustrated below.

即ら該富化器として、大気を取り入れるためのファン手
段、その大気が気体選択透過性膜の表面を通過し酸素富
化空気が透過するように構成された多数の膜セルからな
るモジュール、該膜セルにおける膜裏面側を大気よりも
低い圧力に保ち、且つ酸素富化空気をモジュールより取
り出すための真空ポンプ手段、及び取り出された酸素富
化空気を該富化器の出口に流通せしめる富化器内導管手
段を具備したものが挙げられる。また本発明の他の好ま
しい態様の1つである吸着型酸素富化器の具体例として
、窒素ガスを選択的に吸着する吸着剤を充填した吸着剤
床を2M、該吸着剤床に加圧された大気を流入するため
のコンプレッサ一手段。
That is, the enricher is a module consisting of a fan means for taking in atmospheric air, a number of membrane cells configured so that the atmospheric air passes through the surface of a gas selectively permeable membrane, and oxygen-enriched air permeates therethrough; A vacuum pump means for maintaining the back side of the membrane in the membrane cell at a pressure lower than that of the atmosphere and taking out the oxygen-enriched air from the module, and an enrichment means for making the taken-out oxygen-enriched air flow to the outlet of the enricher. Examples include those equipped with internal conduit means. Further, as a specific example of the adsorption type oxygen enricher which is one of the other preferred embodiments of the present invention, an adsorbent bed filled with an adsorbent that selectively adsorbs nitrogen gas is placed at 2M, and the adsorbent bed is pressurized. A compressor means for inflowing the atmosphere.

及び該吸着剤床から酸素富化空気を取り出し出口に流通
せしめるための富化器内導管手段を具備したものであっ
て、2基の吸着床が交互に加圧−減圧−再生のサイクル
を繰り返すように運転される富化器が挙げられる。尚い
ずれの富化器においても、酸素富化空気を富化器の出口
に流通せしめるための導管手段において、供給する酸素
富化空気の流量を調節する手段を有することが望ましい
。
and an enrichment conduit means for extracting oxygen-enriched air from the adsorbent bed and distributing it to the outlet, the two adsorption beds alternately repeating the pressurization-depressurization-regeneration cycle. An example is an enricher that is operated as follows. In any of the enrichers, it is desirable that the conduit means for passing the oxygen-enriched air to the outlet of the enricher include means for adjusting the flow rate of the supplied oxygen-enriched air.

次に実施例をあげて本発明をさらに詳細に説明する。Next, the present invention will be explained in more detail with reference to Examples.

実施例1 吸着型酸素富化器(帝人製ハイサンソ)で加湿器(水充
填部の内径55sφ)を付加したものを用いて、加湿さ
れた2ρ7m1nの酸素富化空気を取り出し、第1表に
示した平均細孔径のテフロン製フィルターに通過せしめ
、その通過後の空気の湿度及び水滴の有無を調べた結果
を第1表に合わせて示す。
Example 1 Humidified oxygen-enriched air of 2ρ7ml was taken out using an adsorption type oxygen enricher (Hisanso manufactured by Teijin) with a humidifier (inner diameter of water filling part: 55sφ), and the oxygen enriched air was extracted as shown in Table 1. Table 1 shows the results of testing the humidity and presence of water droplets after passing through a Teflon filter with an average pore size of

表1表 (以下余白) 〈発明の効果〉 本発明は、水滴及び異臭を含有した気体中からその水滴
及び異臭を除去し得る簡単で軽量な気体浄化器及び特定
の気体浄化器を備えた酸素富化気体供給装置を提供する
ものである。特に該装置にあっては、それから供給され
る酸素富化空気が水滴や異臭を含まず清浄なものであり
、それを使用する者にとって不快感がないという優れた
利点がある。
Table 1 (blank below) <Effects of the Invention> The present invention provides a simple and lightweight gas purifier capable of removing water droplets and odor from a gas containing them, and an oxygen purifier equipped with a specific gas purifier. An enriched gas supply device is provided. In particular, this device has the advantage that the oxygen-enriched air supplied therefrom is clean, free of water droplets and odor, and does not cause discomfort to the person using it.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は、本発明に係る酸素富化気体供給装置の実施態
様を模式的に例示したものである。第2図は、本発明に
係る気体浄化器の実施態様を断面図で例示したものであ
る。
FIG. 1 schematically illustrates an embodiment of an oxygen-enriched gas supply apparatus according to the present invention. FIG. 2 is a sectional view illustrating an embodiment of the gas purifier according to the present invention.

Claims (7)

【特許請求の範囲】[Claims] (1)気体の入口及び出口を具備した容器内にフィルタ
ーと吸着剤層を直列に配した気体浄化器。
(1) A gas purifier in which a filter and an adsorbent layer are arranged in series in a container equipped with a gas inlet and outlet.
(2)酸素富化気体の発生手段と、該発生手段から離れ
た所に位置した該酸素富化気体を使用に供する供給手段
と、該発生手段から該供給手段に該酸素富化気体を導く
ための導管手段を有した酸素富化気体供給装置であって
、該導管手段の途中にフィルター及び/又は吸着剤を具
備した気体浄化手段を有したことを特徴とする酸素富化
気体供給装置。
(2) a means for generating an oxygen-enriched gas, a supply means for providing the oxygen-enriched gas located at a location away from the generation means, and guiding the oxygen-enriched gas from the generation means to the supply means; What is claimed is: 1. An oxygen-enriched gas supply device comprising a conduit means for the purpose of cleaning, the conduit means having a gas purification means provided with a filter and/or an adsorbent in the middle of the conduit means.
(3)該フィルターの平均孔径が0.8μ以下である特
許請求の範囲第2項記載の装置。
(3) The device according to claim 2, wherein the filter has an average pore diameter of 0.8 μm or less.
(4)該フィルターの少くとも一方の面が撥水性を有す
るものである特許請求の範囲第2項記載の装置。
(4) The device according to claim 2, wherein at least one surface of the filter is water repellent.
(5)該気体浄化手段が、フィルターと吸着剤を直列に
配して同一容器内に収納せしめたものである特許請求の
範囲第2項記載の装置。
(5) The device according to claim 2, wherein the gas purifying means comprises a filter and an adsorbent arranged in series and housed in the same container.
(6)該酸素富化気体の発生手段が、膜型酸素富化器、
吸着型酸素富化器及び酸素ボンベの少くとも1種を用い
たものである特許請求の範囲第2項記載の装置。
(6) The means for generating the oxygen-enriched gas is a membrane-type oxygen enricher,
The apparatus according to claim 2, which uses at least one of an adsorption type oxygen enricher and an oxygen cylinder.
(7)該発生手段が加湿器を具備したものである特許請
求の範囲第6項記載の装置。
(7) The device according to claim 6, wherein the generating means is equipped with a humidifier.
JP18588585A 1985-08-26 1985-08-26 Gas purifier and oxygen enriched gas feeder Granted JPS6247371A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP18588585A JPS6247371A (en) 1985-08-26 1985-08-26 Gas purifier and oxygen enriched gas feeder

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP18588585A JPS6247371A (en) 1985-08-26 1985-08-26 Gas purifier and oxygen enriched gas feeder

Publications (2)

Publication Number Publication Date
JPS6247371A true JPS6247371A (en) 1987-03-02
JPH0312901B2 JPH0312901B2 (en) 1991-02-21

Family

ID=16178579

Family Applications (1)

Application Number Title Priority Date Filing Date
JP18588585A Granted JPS6247371A (en) 1985-08-26 1985-08-26 Gas purifier and oxygen enriched gas feeder

Country Status (1)

Country Link
JP (1) JPS6247371A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08187300A (en) * 1995-01-05 1996-07-23 Pai-Hee Mou Respiratory assisted life saver
JP2014221204A (en) * 2008-01-28 2014-11-27 ゲノ エルエルシー Transformation from nitrogen dioxide (no2) to nitric monoxide (no)
US11202880B2 (en) 2004-08-18 2021-12-21 Vero Biotech LLC Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11554241B2 (en) 2004-08-18 2023-01-17 Vero Biotech Inc. Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11744978B2 (en) 2008-08-21 2023-09-05 Vero Biotech Inc. Systems and devices for generating nitric oxide
US11925764B2 (en) 2009-06-22 2024-03-12 Vero Biotech Inc. Nitric oxide therapies

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60118605A (en) * 1983-11-25 1985-06-26 Matsushita Seiko Co Ltd Oxygen concentrator

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60118605A (en) * 1983-11-25 1985-06-26 Matsushita Seiko Co Ltd Oxygen concentrator

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH08187300A (en) * 1995-01-05 1996-07-23 Pai-Hee Mou Respiratory assisted life saver
US11202880B2 (en) 2004-08-18 2021-12-21 Vero Biotech LLC Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11291793B2 (en) 2004-08-18 2022-04-05 Vero Biotech Inc. Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11383059B2 (en) 2004-08-18 2022-07-12 Vero Biotech Inc. Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11554241B2 (en) 2004-08-18 2023-01-17 Vero Biotech Inc. Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
JP2014221204A (en) * 2008-01-28 2014-11-27 ゲノ エルエルシー Transformation from nitrogen dioxide (no2) to nitric monoxide (no)
US11312626B2 (en) 2008-01-28 2022-04-26 Vero Biotech Inc. Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11884541B2 (en) 2008-01-28 2024-01-30 Vero Biotech Inc. Conversion of nitrogen dioxide (NO2) to nitric oxide (NO)
US11744978B2 (en) 2008-08-21 2023-09-05 Vero Biotech Inc. Systems and devices for generating nitric oxide
US12171948B2 (en) 2008-08-21 2024-12-24 Vero Biotech Inc. Systems and devices for generating nitric oxide
US11925764B2 (en) 2009-06-22 2024-03-12 Vero Biotech Inc. Nitric oxide therapies

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